Rapid action coater and process for coating ceramic particles using same
View Patent ↗A new device and process for continuously applying coatings, such as resin and additives or polymers or the like, to minerals are disclosed. The device and apparatus differ substantially from standard batch coating processes currently used by industry. The apparatus uses a horizontal cylinder with an internal auger and a series of injection ports distributed along the cylinder. Minerals that are to be coated are pretreated and passed through the mixing cylinder using the auger (which may comprise one or more screws with variable pitch blades). As the mineral particles pass through the cylinder various coating materials are injected by the injection ports. The complete system is described, the method of use is explained and the control system which allows for different products is described.
1. A continuous process for producing resin coated ceramic particles comprising
feeding ceramic particles heated to a temperature above the melting point of the resin into an inlet of a mixing zone and withdrawing resin coated particles from an outlet of the mixing zone in a manner such that the particles travel along a travel path essentially continuously from the inlet to the outlet,
combining a resin with the ceramic particles in the mixing zone at a first location along the travel path,
mixing the resin and particles in the mixing zone, thereby causing the resin to melt and encapsulate the individual particles as they move along the travel path,
combining a curing agent for the resin with the ceramic particles and the resin in the mixing zone at a second location along the travel path downstream of the first location, and
cooling the resin encapsulated particles to a temperature below the melting point of the resin, thereby producing an essentially free flowing mass of resin coated particles at the outlet of the mixing zone,
wherein the mixture of resin and particles is moved through the mixing zone by at least one auger comprising a rotating shaft and multiple paddles connected thereto, some of the paddles being arranged with reverse pitch to cause backward travel of the mixture in a portion of the mixing zone, thereby increasing the residence time of the mixture in the mixing zone.
2. The process of claim 1 , wherein the at least one auger is essentially horizontal.
3. The process of claim 2 , wherein the mixture of resin and particles is moved through at least a portion of the mixing zone by at least two augers, each auger comprising a rotating shaft and multiple paddles connected thereto, the augers being arranged generally adjacent to one another in a manner so that, as the augers rotate, the paddles of adjacent augers mechanically clear one another yet overlap one another when viewed in the axial direction of the augers.
4. The process of claim 3 , wherein the mixing zone is divided into at least three mixing zone segments, wherein in each mixing zone segment resin and then curing agent are separately added to the particles in that mixing zone segment to produce a resin coating on the particles, and wherein the at least three mixing zone segments are arranged in series with respect to one another so that the resin coating produced in each successive mixing zone segment is applied to the coating produced in the preceding mixing zone segment.
5. The process of claim 4 , wherein the resin is in solid particulate form when fed to the mixing zone, and further wherein the resin encapsulated particles are cooled below the melting point of the resin by contact with a liquid before being withdrawn from the mixing zone.
6. The process of claim 5 , wherein the resin is a phenolic resin and the curing agent is hexamethylenetetramine.
7. The process of claim 6 , wherein the resin encapsulated particles are cooled to a temperature below the curing temperature of the resin so that the resin coating on the ceramic particles is a B-stage phenolic resin.
8. The process of claim 7 , wherein a resin coated proppant is produced.
9. The process of claim 7 , wherein a resin coated foundry sand is produced.
10. The process of claim 1 , wherein the mixing zone is divided into at least three mixing zone segments, wherein in each mixing zone segment resin and then curing agent are separately added to the particles in that mixing zone segment to produce a resin coating on the particles, and wherein the at least three mixing zone segments are arranged in series with respect to one another so that the resin coating produced in each successive mixing zone segment is applied to the coating produced in the preceding mixing zone segment.
11. The process of claim 10 , wherein the resin is in solid particulate form when fed to the mixing zone, and further wherein the resin encapsulated particles are cooled below the melting point of the resin by contact with a liquid before being withdrawn from the mixing zone.
12. The process of claim 11 , wherein the resin is a phenolic resin and the curing agent is hexamethylenetetramine.
13. The process of claim 12 , wherein the resin encapsulated particles are cooled to a temperature below the curing temperature of the resin so that the resin coating on the ceramic particles is a B-stage phenolic resin.
14. The process of claim 13 , wherein a resin coated proppant is produced.
15. The process of claim 13 , wherein a resin coated foundry sand is produced.
16. The process of claim 10 , wherein the mixture of resin and particles is moved through at least a portion of the mixing zone by at least two augers, each auger comprising a rotating shaft and multiple paddles connected thereto, the augers being arranged generally adjacent to one another in a manner so that, as the augers rotate, the paddles of adjacent augers mechanically clear one another yet overlap one another when viewed in the axial direction of the augers.
17. The process of claim 1 , wherein mixing of the resin and particles causes a mixture of resin and particles to form in the mixing zone, wherein the pitch of the paddles is arranged to move this mixture forward through the mixing zone, and further wherein some of the paddles are arranged with a reverse pitch for driving the mixture backwards in the mixing zone, thereby increasing the residence time of the mixture inside the mixing zone.
18. The process of claim 17 , wherein the paddles are arranged so that the mixture travels forward and backward in combination.
19. The process of claim 17 , wherein the paddles are arranged so that the mixture travels forward down the travel path inside the mixing zone to the location of the paddles arranged with reverse pitch where the mixture reverses direction and hits additional mixture traveling forward in the mixing zone, thereby increasing the residence time of the mixture inside the mixing zone.